AU593318B2 - Polyethersulfone plus reinforcing fibre - Google Patents

Polyethersulfone plus reinforcing fibre Download PDF

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AU593318B2
AU593318B2 AU67949/87A AU6794987A AU593318B2 AU 593318 B2 AU593318 B2 AU 593318B2 AU 67949/87 A AU67949/87 A AU 67949/87A AU 6794987 A AU6794987 A AU 6794987A AU 593318 B2 AU593318 B2 AU 593318B2
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composition
mixture
units
polysulphone
fibre
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AU6794987A (en
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Frederic Neil Cogswell
Michael Kenneth Cox
David Colin Leach
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Imperial Chemical Industries Ltd
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Imperial Chemical Industries Ltd
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    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08LCOMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L81/00Compositions of macromolecular compounds obtained by reactions forming in the main chain of the macromolecule a linkage containing sulfur with or without nitrogen, oxygen or carbon only; Compositions of polysulfones; Compositions of derivatives of such polymers
    • C08L81/06Polysulfones; Polyethersulfones
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J5/00Manufacture of articles or shaped materials containing macromolecular substances
    • C08J5/04Reinforcing macromolecular compounds with loose or coherent fibrous material
    • C08J5/0405Reinforcing macromolecular compounds with loose or coherent fibrous material with inorganic fibres
    • C08J5/042Reinforcing macromolecular compounds with loose or coherent fibrous material with inorganic fibres with carbon fibres
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08LCOMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L71/00Compositions of polyethers obtained by reactions forming an ether link in the main chain; Compositions of derivatives of such polymers
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J2381/00Characterised by the use of macromolecular compounds obtained by reactions forming in the main chain of the macromolecule a linkage containing sulfur with or without nitrogen, oxygen, or carbon only; Polysulfones; Derivatives of such polymers
    • C08J2381/06Polysulfones; Polyethersulfones

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  • Chemical & Material Sciences (AREA)
  • Health & Medical Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Medicinal Chemistry (AREA)
  • Polymers & Plastics (AREA)
  • Organic Chemistry (AREA)
  • Inorganic Chemistry (AREA)
  • Engineering & Computer Science (AREA)
  • Manufacturing & Machinery (AREA)
  • Materials Engineering (AREA)
  • Reinforced Plastic Materials (AREA)
  • Compositions Of Macromolecular Compounds (AREA)

Description

PHILLIPS ORMONDE AND FITZPATRICK Patent and Trade Mark Attorneys 367 Collins Street Melbourne, Australia P17/2/83 i
AUSTRALIA
Patents Act COMPLETE SPECIFICATION
(ORIGINAL)
Class Int. Class Application Number: Lodged: 6 71' 116 Complete Specification Lodged: Published: Priority o 99 99 0 98 9 999 ii
I,~
Related Art: APPLICANT'S REF.: H33745/AU IMPERIAL CHEMICAL INDUSTRIES PLC Name(s) of Applicant(s): t c t tt r Ir SAddress(es) of Applicant(s): Actual Inventor(s): t Actual Inventor(s): c9c t t Imperial Chemical House, Millbank, London, SW1P 3JF United Kingdom FREDRIC NEIL COGSWELL MICHAEL KENNETH COX DAVID COLIN LEACH Address for Service is: PHILLIPS, ORMONDE AND FITZPATRICK SPatent and Trade Mark Attorneys 4 367 Collins Street V E Melbourne, Australia, 3000 Complete Specification for the invention entitled: F-ly"e-k.slLt LP .e us:. rec2 i b e- The following statement is a full description of this invention, including the best method of performing it known to applicant(s): P19/3/84 i 1 la- H 33745 The present invention relates to a polymer composition, in particular containing a polyarylether derivative and a fibrous reinforcing agent.
Among polyarylether derivatives having good high temperature properties, polyarylethersulphones are generally amorphous but have glass transition temperatures whic' may be over 200°C, and polyaryletherketones are generally crystalline but typically have glass transition temperatures below 200 0 C, for example between 140°C and 165°C. Some polyaryletherketones have glass transition temperatures of about 200°C, but typically these have melting points close to or even above 400 0 C and thus have to be processed at a temperature close to that at which rapid degradation occurs.
Polyarylether derivative compositions containing fibrous *a*O 15 reinforcing agents, as described for example in EPA 31198, have a o0 oo.. high flexural modulus and high heat deflection temperature but show 0" a marked deterioration at above the glass transition temperature; and 0 00 0 o many such compositions based on polyaryletherketones show the 00 a deterioration at considerably below 200 0 C, typically at between 140°C 20 and 165 0
C.
We have now found that a polymer composition based on a particular range of copolymers has improved retention of mechanical properties at temperatures above 200 0
C.
o According to the invention a polymer composition comprises: component a) which is at least one aromatic polysulphone, containing the repeating units Ph S02 Ph -Ph h SO2 Ph I and 30 Ar II (where Ph is phenylene and Ar is a divalent aromatic radical) linked Stogether through ether linkages, in a relative molar proportion of the units I II in the range 25 75 to 60 40; and component b) which is 5 to 80% by weight of a fibrous reinforcing agent calculated on the total of a) and b).
Ph is preferably para-phenylene. Ar may be a mono-or poly- 1. i i i- '1 ULL' -I i i I- i i -li-~i 2 H 33745 radical such as phenylene or biphenylene, but is preferably one in which aromatic groups are linked together through non-aromatic groups.
More specifically Ar is Arl Z Arl where each Arl, which may be the same or different, is a divalent aromatic hydrocarbon radical; and Z is selected from SO SO 2 CO and divalent aliphatic hydrocarbon radicals.
Arl may be a mono- or poly- radical and is preferably phenylene, especially para-phenylene.
We particularly prefer that in component a) the repeating units are
*OP
09 4
P.,
P
o P
OPOI
Ph I
SO
2 Ph 1 PhI SO 2 PhI Ph' S02 Ph 1 20 where Ph' is para-phenylene.
The ether linkage may link together two units I, or two units II or a unit I to a unit II.
In any particular polysulphone there may be a plurality of 25 different units II satisfying the definition Ar, but preferably units C t II are the same in any particular polymer; a mixture of polysulphones each having a different unit II may be used.
«c If component a) of the composition is a mixture of polysulphones, it preferably consists of two of them, one containing only units II or IIA, the other containing both units; and the mixture should nonetheless contain units I and II in the relative molar proportions 25:75 to 60:40 respectively. Thus the mixture may for example contain 50% molar each of a polymer containing only units II and of a polymer containing units I and II in the relative molar proportions 50:50. If a mixture of polysulphones is used as component it preferably is either a polymer containing r i -B m
I
3 H 33745 only units II (preferably under 20% by weight) mixed with one containing units I and II in the relative molar proportions I:II in the range 25:75 to 60:40, or else is a mixture of polymers each of which contains units I and II in the relative molar proportions I:II in the range 25:75 to 60:40. In any such systems the preferred range is 25:75 to 50:50.
We have obtained useful results when component a) is a single polysulphone containing units IA and IIA in equimolar proportions.
We prefer that the polysulphone or mixture have a reduced viscosity measured as a 1% by weight solution in N,N-dimiethylformamide at 25 0 C, of at least 0.05 and preferably not more than 2.0. Particularly preferred polysulphones have RV in the range 0.2 to 1.0 especially 0.3 to 0.8.
The fibrous reinforcing agent can be organic or inorganic such 0 0 .o o as poly-paraphenylene terephthalamide fibre, glass fibre or, preferably, carbon fibre. It may be added as short or chopped fibre S which typically has a mean fibre length of only a few centimetres, particularly not more than 2 cm, for example about 6mm. Using such i o e* 20 fibre, the composition typically contains 5 to 35, preferably at least by weight of fibrous reinforcing agent. For structural applications, it is preferred to use a continuous fibrous material, S, for example glass or carbon, especially 30 to 70, more especially to 70, by volume thereof.
The composition may contain one or more other materials, for example organic and inorganic fillers such as polytetrafluoroethylene, graphite, boron nitride, mica, talc and vermiculite; nucleating agents; and stabilisers such as phosphates. The total of such materials and fibrous reinforcing agent, should be such that the 30 composition contains at least 20% by volume of the polysulphone or mixture.
SThe composition may be made by mixing the polysulphone or Smixture with the fibrous reinforcing agent and, if required, other materials, by for example particle or melt blending.
More specifically the polysulphone or mixture in the form of a dry powder or granules can be mixed with the fibrous reinforcing agent and, if required, the other materials, using a technique such as r- 4 H 33745 tumble blending or a high speed mixer. The blend thus obtained may be extruded into a lace which is chopped to give granules. The granules can be used to produce shaped articles by for example injection moulding or extrusion.
Alternatively the composition may be made by passing the fibrous reinforcing agent as an essentially continuous fibre, for example of glass or carbon, into contact with a melt formed from the polysulphone or mixture. The composition, now in the form of filaments (fibres) of the fibrous reinforcing agent impregnated with the polysulphone or mixture, may be used alone or together with other materials, for example a further quantity of the same or a different polysulphone or mixture, to form a shaped article. This technique is described in more detail in EP-A 56703, 102158 and 102159.
Yet a further technique of producing the composition 15 comprises making a solution of the polysulphone or mixture and contacting the fibrous reinforcing agent therewith. Suitable solvents include dichloromethane, N,N-dimethylformamide, dimethylsulphoxide, and N-methyl-2-pyrrolidone. The fibrous reinforcing agent may be u" stirred with the solution, separated and dried to remove the solvent.
20 An essentially continuous fibre may be passed through a vessel containing the solution and then through a heated zone to evaporate off the solvent. The solution typically contains 1 to 20, preferably 2 to 10, g of polysulphone for each 100 cm 3 of solution. This is not a particularly preferred technique since it is difficult to totally remove the solvent and the presence of solvent can adversely affect the properties of the composition.
In a yet further procedure the polysulphone or mixture in film form is laminated to the fibrous reinforcing agent which may be in the form of a non-woven mat of relatively short fibres, a woven 30 cloth or essentially continuous fibre. The film may be formed by casting from solution but more preferably by melt extrusion, for example by extruding through a slot die and drawing off the extruded film over rollers. Such lamination of film to fibre is effected under conditions of temperature and pressure sufficient to cause the polysulphone or mixture to flow and impregnate the fibres, preferably at least 320°C and typically in the range 340°C to 420 0 C, and at a I i 5 H 33745 pressure of at least 0.1, preferably at least 10, MN/m 2 Lamination is conveniently effected using at least one pair of heated rollers.
Each polysulphone of component of the composition can be prepared by an electrophilic process but is conveniently prepared by a nucleophilic process.
Nucleophilic processes for preparing such polysulphones are described, inter alia, in GB-A 1078234, 1153053, 1397260, 1558671, 1569602, and 1586972 and Canadian 847963. Polysulphones containing units I and the preparation thereof are described in GB-A 1397260 and in Polymer, 18 (1977) pages 359 to 364 and 369 to 374.
The polysulphones are preferably prepared by polycondensation of at least one aryl dihalide with at least one bisphenol, or of at least two different halophenols. The polycondensation can be effected by forming a metal phenate, particularly an alkali metal co 15 phenate, for example by reaction with an alkali metal hydroxide, Oo adding dihalide and thereafter heating the reaction mixture to polycondensation temperature, typically at least 150 0 C. The o t polycondensation is preferably in the presence of an alkali metal "carbonate or bicarbonate or a mixture thereof. It is also preferably 0 in the presence of a solvent, for example diphenyl sulphone or a substituted derivative thereof. The temperature is conveniently between 150°C and 400°C, with a final temperature preferably in the range 280°C to 320 0
C.
The polysulphones are conveniently prepared by the S polycondensation of compounds of the formulae
X
1 Ph S02 Ph Ph S0 2 Ph X 2
III
and c
X
3 Ar X 4
IV
in the molar proportions of III IV in the range from 25:75 to 60:40.
wherein Ph and Ar are as hereinbefore defined, and
X
1
X
2
X
3 and X 4 are each a halogen or OH i 6 H 33745 where the proportions of III and IV and the nature of the groups X 1
X
2
X
3 and X 4 are such that halogen and OH are in essentially stoichiometric proportions. If X 3 and/or X 4 are halogen they are activated by a group SO -SO 2 or -CO -in the ortho or preferably para-position thereto. Preferred polysulphones are prepared using 4,4'-bis (4-chlorophenylsulphonyl) biphenyl as compound III and 4,4'-dihydroxydiphenyl-sulphone or a mixture of and 4,4'-dichlorodiphenyl-sulphone as compound IV. The proportions of compound and are from 1:2:1 to 2:2:0.
Essentially stoichiometric proportion embraces a small excess of dihalide or bisphenol for example up to 5% molar, and it is particularly preferred to use excess dihalide.
Filament (fibres) of the fibrous reinforcing agent impregnated with the polysulphone or mixture especially those made by the procedure of one or more of EP-A 56703, 102158 and 102159, Scan be laminated together by the application of heat and pressure, for Sexample by compression moulding or by heated rollers, at a temperature above the glass transition temperature of the polysulphone or mixture, conveniently at least 320 0 C and typically about 400 C, and at a S 20 pressure in particular at least 0.1, preferably at least 5,MN/m 2 The composition, particularly one obtained using an essentially 0 o continuous fibrous reinforcing agent, may be formed into a multi-ply laminate. This may be anisotropic in which the fibres are oriented S* essentially parallel to one another or quasi-isotropic in each ply of which the fibres are oriented at an angle, conveniently 450 as in most quasi-isotropic laminates but possibly for example 300 or 60° or 900 or intermediately, to those in the plies above and below.
Orientations intermediate between anisotropic and quasi-isotropic, and combination laminates, are also provided. Suitable laminates contain 30 at least.4 preferably at least 8, plies. The number of plies is dependent on the application for the laminate, for example the strength required, and laminates containing 32 or even more, for example several hundred, plies may be desirable.
In a particularly preferred composition the polysulphone contains the repeating units IA and IIA in essentially equimolar proportions and the fibrous reinforcing agent is essentially continuous carbon fibre. Mouldings or, particularly, laminates formed therefrom show at a temperature up to 240 0 C a deterioration of less than 30% in flexural modulus as measured at 23 0 C. Furthermore, -7 H 33745 although this polysulphone is amorphous, the composition has an environmental resistance superior to that of many other amorphous polymers. Thus after exposure to water at 100°C for 14 days such a composition showed a gain in weight of less than essentially unaffected tranverse flexural strength and short-beam shear strength Furthermore, after exposure to a hydraulic fluid at 70 0 C for 14 days, Sa similar composition showed only a slight weight loss (less than 0.2% by weight), essentially unaffected short-beam shear strength and transverse flexural strength decreased by less than Further details of the invention are set out by way of illustration in the following examples.
Example 1 A polysulphone containing the above-mentioned units IA and IIA in essentially equimolecular proportions, linked together through 1 15 ether linkages and having a reduced viscosity of 0.37 measured at using a 1.0% by weight solution in 100 cm 3 of a solution in N,N- '"dimethylformamide, was dry blended with diphenylsulphone by tumbling in a closed container in a 1:1 weight ratio.
25 collimated tows of continuous carbon fibres ("Magnamite" 20 AS-4 supplied by Hercules Inc of Delaware, USA), each tow containing about 12000 individual filaments, were drawn at a rate of 300 mm/minute over a series of stationary guide bars to provide a band of width about 150 mm having a tension of about 50 kg. When the fibres had been guided into contiguous relationship they were pulled over a t in series of 4 fixed, heated, cylindrical bars of 12.6 mm diameter s maintained at 390 0 C. The powder mixture of polymer and diphenyl sulphone was fed to the nip formed between the carbon fibre band and the first fixed cylindrical bar. The powder melted rapidly to provide a melt pool in the nip which impregnated the fibre band passing over S' 30 the bar. The structure was passed over and under the three further heated bars without the addition of further of the polymer mixture.
Provision was made for extracting the fumes of diphenyl sulphone which were evolved. The product obtained was a continuous tape, 150 mm wide and about 0.125 mm thick containing 60% by weight (53% by volume) of the carbon fibre which had been well wetted by the polymer.
I
-8 H 33745 Anisotropic Laminates Formation Sections cut from the tape were laminated together by compression moulding at 400'C for five minutes at an applied pressure of 10 MN/rm 2 then cooled to about 80'C, still in the press and under pressure, using air and then water, to give a cooling rate of about per minute. Sixteen thicknesses of the tape were laid up to give uniaxial alignment of the carbon fibre laminate of thickness about 2 mm.
Mechanical Properties In Table One are given the results of at various temperatures.
Table One mechanical testing o 9e 90 .000 0900 0 *0 0 0* 0*t o Ge 0 000 S 0*
S
0 Z~,t *9 0 0 a.
*4St Ot t I Temp I Longitudinal Flexure I Transverse Flexure SBSS I Modulus I Strength I Modulus I Strength I (c) I I (GN/m 2 I (MN/m 2 I (GN/m 2 I (MN/m 2 I(MN/m 2 1 23 1 ill 1 1450 1 7.1 1 91 1 76 1 80 1 114 1350 1 6.5 1 66 1 69 120 1 ND ND 1 6.5 1 61 1 61 1 180 114 1150 1 6.0 1 48 1 48 240 1 82 1 300 1 3.0 1 13 1 29 Notes to Table One Longitudinal Flexure was measured by Method D 790-80, using a 100 mm span. ND the technique of ASTM Test means not determined.
tt t t t C 0 t Transverse Flexure was measured by the technique of ASTM Test Method D790-80, using a 40 mm span.
SBSS is short beam shear strength and is determined by the technique of ASTM Test Method D2344-72, using a span to sample thickness ratio of 5:1.
I
ii*^ -9 H 33745 Environmental resistance Samples of the laminates subjected to hot water, others to a hydraulic fluid ("Skydrol" grade LD4, available from Monsanto Chemical). The weight of the laminates and their mechanical properties were determined before and after. The results are set out in Table Two.
Table Two SEnvironment Weight Transverse flexural SBSS i change I Strength retention I retention I S Water 0.47 100 S Skydrol 0.09 73 100
I
a.rr c c
I
Notes to Table Two and are both as defined in Notes to Table One.
Water means water at 100°C for 14 days. Skydrol means hydraulic fluid ("Skydrol" grade LD4) at 70°C for 14 days.
Weight change is given as a percentage of the original weight.
indicates a weight gain. indicates a weight loss.
Retention is expressed as a percentage of the original measurement.
Comparative Example 30 Using the procedure as described in Example 1, a composition was formed from a polysulphone having only units IIA namely 'Victrex' (Registered Trade Mark) PES (polyarylethersulphone) aromatic polymer 5200 P grade, obtainable from Imperial Chemical Industries PLC and having a reduced viscosity of 0.52. The polymer to diphenylsulphone ratio was 1:1 by weight.
r St r f
C
10 H 33745 Some samples of laminates made therefrom as described in Example 1 were subjected to water, others to Skydrol. Test results are set out in Table Three.
Table Three Environment Weight Transverse flexural I SBSS I change strength retention I retention[ I 1 Water I 0.38 93 1 94 ISkydrol 0.03 66 I 99 Notes to Table Three and are both as defined in Notes to Table One and are all as defined in Notes to Table Two.
From a comparison of the results set out in Tables Two and Three it will be seen that the composition of Example 1 shows *a 20 resistance to water and hydraulic fluid superior to that of the composition of the Comparative Example. This is particularly evident in respect of the retention of tranverse flexural strength, which property is the most sensitive to any defects in the polymer composition.
25 Example 2 The procedure of Example 1 was repeated with the exception that the polymer to diphenylsulphone weight ratio was 1:2 and the composition contained 73% by weight (65% by volume) of carbon fibre.
Example 3 A quasi-isotropic laminate was made by laying up 16 thicknesses of tape from Example 1, with a 450 angle between successive plies, then uniting them by compression moulding as in Example 1. It was tested for impact resistance at various temperatures by the method of C J Hooley and S Turner (Mechanical Testing of Plastics, Institute of Mechanical Engineers, June/July 1979, Automotive Engineer), using a falling weight dart 12.7 mm in diameter and a 75 mm square specimen resting unclamped on a 50 mm support ring. The levels of energy absorbed in effecting a standard area of damage are shown in Table Four.
-i 't; 11 H 33745 Table Four I Temp oC I Energy absorbed J, to I Total energy I___maximum force I absorbed, J 1
I
S -55 1 6.0 19.2 I 23 1 5.9 I 21.2 I 70 1 5.7 21.9 Example 4 The laminates preparation described in Example 1 was repeated using a different batch of the polymer and with 68% w/w of the fibre.
The products were tested in the same way at various temperatures, but excluding transverse flexure modulus. In addition, a anisotropic laminate panel was made and tested by the method of ASTM D695-85, which involves machining the panel perpendicularly to the fibres with a 6 mm wide rectangular groove on each side leaving a 1 mm thick central planar region, then measuring compressive strength by 20 applying force to panel in the direction of the fibres. Results are shown in Table Five.
Table Five It C. 1I Temp I Longitudinal Flexure Transverse I SBSS ICompressive I Vt' e 25 (OC) I Modulus I Strength I Flexure (b)J I Strength I I I I Strength I S_ I (GN/m 2 I (MN/m 2 I (MN/m 2 I(MN/m 2 )1 (MN/m2) SI I I I I 3 -55 1 120 1 1300 I 102 I 79 I 1549 1 1 23 1 119 1 1208 1 81 i 63 1 1324 1 1 80 1 118 I 1044 58 1 53 1 1176 1 1 160 1 116 I 793 I 46 1 42 1 1137 I S 180 1 115 I 744 1 41 1 33 1 1134 1 S 200 I 117 1 644 1 34 1 23 I 1043 1 1 220 I 98 1 305 I 33 I 14 1 ND I Notes Suffixes and have the same meaning as for Table One.

Claims (9)

1. A polymer composition comprising component a) which is at least one aromatic polysulphone, containing the repeating units -Ph -SO 2 Ph -Ph SO Ph I and Ar II where Ph is a phenylene; and Ar is a divalent aromatic radical linked together through ether linkages, in a relative molar proportion I :II in the range 25 75 to 60 40; and component b) which is 5 to 80% by weight of a fibrous reinforcing agent, calculated on the total of a) and b). o 2. A composition as claimed in claim 1 in which t'p Ar is a divalent mono- or poly- radical or a group 1 1 1 -Ar Z Ar in which each Ar which may be the same or different, is a divalent aromatic hydrocarbon radical; and Z is selected from SO -SO -CO and 2 divalent aliphatic hydrocarbon radicals.
3. A composition as claimed in claim 2 in which component a) contains units 1 1 1 1 S- Ph SPh h Ph -SO Ph IA 2 2 and 1 1 Ph S0 Ph IIA where Ph is para-phenylene.
4. A composition as claimed in any one of claims 1 to 3 r in which component a) is a single polysulphone having both S units IA and IIA in its molecule; or is mixture of polysulphones each having a different unit II; or is a mixture of two polysulphones one of which contains only units I'l and the other contains both units I and II; or is a i CL'A^N -l9t \-4,A applicant(s): P19/3/84 1 -13- mixture in which at least one polymer contains units I and II in the relative molar proportions I II of 25 75 to A composition as claimed in any one of claims 1 to 4 in which the polysulphone or mixture has a reduced viscosity in the range 0.05 to 2.0, preferably in the range 0.2 to
6. A composition as claimed in any one of claims 1 to in which the range of proportion of the two units is 25:75 to 50:50.
7. A composition as claimed in any one of claims 1 to 6 comprising polysulphone containing the repeating units Ph -SO Ph Ph SO Ph IA and Ph SO Ph IIA 2 in essentially equimolar properties and essentially continuous carbon fibre. S 8. A composition according to any one of the preceeding claims and having the form of collimated continuous polymer impregnated fibre tape.
9. A laminate formed from a composition as claimed in any S one of claims 1 to 7. A process for the production of a composition which comprises mixing a) a polysulphone or mixture containing the repeating units Ph SO -Ph Ph SO Ph I 2 2 and Ar II where Ph is phenylene; and Ar is a divalent aromatic radical L linked together through ether linkages, in the relative molar proportions of units I units II, in the range from 25 to 60 40; with b) 5 to 80% by weight of fibrous reinforcing agent, calculated on the total of a) and by passing a continuous fibrous reinforcing agent into contact with a melt formed I -14- from at least one polysulphone or mixture.
11. A process according to claim 10 which comprises a) providing in powder form a mixture of diphenyl sulphone with the polysulphone. b) guiding a band of collimated continuous fibre in contact with a cylindrical bar held at a temperature above the melting point of the mixture; c) feeding the mixture to the nip between the band and the bar, whereby to form a melt pool and to impregnate the fibre.
12. A process as claimed in claim 10 which comprises laminating the composition in the form of impregnated fibres to other impregnated fibres thereof by the application of heat and pressure. 13,. A composition as claimed in claim 1, substantially as hereinbefore described, with reference to any one of the examples.
14. A process as claimed in claim 10, substantially as hereinbefore described with reference to any one of the examples. DATED: 14 November, 1589 PHILLIPS ORMONDE FITZPATRICK Attorneys for: IMPERIAL CHEMICAL INDUSTRIES PLC S 2730N 2730N it t C*.Ef I i CC i"
AU67949/87A 1986-01-30 1987-01-23 Polyethersulfone plus reinforcing fibre Ceased AU593318B2 (en)

Applications Claiming Priority (4)

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GB8602332 1986-01-30
GB8602332 1986-01-30
GB8602828 1986-02-05
GB868602828A GB8602828D0 (en) 1986-02-05 1986-02-05 Polymer composition

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AU593318B2 true AU593318B2 (en) 1990-02-08

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US5219642A (en) * 1989-06-09 1993-06-15 Imperial Chemical Industries Plc Fibre reinforced stuctural thermoplastic composite materials
DE19702590A1 (en) * 1997-01-24 1998-07-30 Basf Ag Thermoplastic molding compounds
JP2016510829A (en) * 2013-03-11 2016-04-11 エオニックス・アドバンスト・マテリアルズ・コーポレイションAonix Advanced Materials Corp. Compositions and methods for producing thermoplastic composites

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GB1337434A (en) * 1970-06-11 1973-11-14 Ici Ltd Polymer composition
US3941748A (en) * 1970-08-19 1976-03-02 Imperial Chemical Industries Limited Process for preparing aromatic polymers in presence of alkali metal fluoride

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JPH08239487A (en) 1996-09-17
EP0235885B1 (en) 1992-08-12
EP0235885A1 (en) 1987-09-09
DE3780984D1 (en) 1992-09-17
DE3780984T2 (en) 1993-03-25
AU6794987A (en) 1987-08-06
JPH0912885A (en) 1997-01-14

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